Method for manufacture of low emissions polypropylene

Patent metadata

Field	Value
Publication number	US-10072105-B2
Application number	US-201515129744-A
Country	US
Kind code	B2
Filing date	Mar 12, 2015
Priority date	Mar 31, 2014
Publication date	Sep 11, 2018
Grant date	Sep 11, 2018

Abstract

The present invention relates to a method for the manufacture of polypropylene having a target melt flow rate of from 10 to 200 g/10 min as determined in accordance with ISO 1133 (230° C., 2.16 kg) comprising the sequential steps of i) polymerizing propylene monomer, and optionally one or more alpha olefin co-monomers so as to form a polypropylene having an initial melt flow rate of from 0.5 to 20 g/10 min (ISO 1133, 230° C., 2.16 kg), ii) visbreaking said polypropylene to obtain polypropylene having said target melt flow rate and wherein the ratio of target to initial melt flow rate is more than 1 iii) maintaining the polypropylene obtained from step ii) at an elevated temperature for a time sufficient to reduce the FOG value of the polypropylene as determined in accordance with VDA 278. The method allows the time for FOG reduction to be reduced as compared to polypropylenes that have the same target melt flow rate, yet which have obtained said melt flow rate without the visbreaking step.

First claim

The invention claimed is:

1. A method for the manufacture of polypropylene having a target melt flow rate of from 10 to 200 g/10 min as determined in accordance with ISO 1133 (230° C., 2.16 kg) comprising the sequential steps of
i) polymerizing propylene monomer, and optionally an alpha olefin co-monomer so as to form a polypropylene having an initial melt flow rate of from 0.5 to 20 g/10 min (ISO 1133, 230° C., 2.16 kg),
ii) visbreaking said polypropylene of step i) to obtain polypropylene having said target melt flow rate and wherein a ratio of target to initial melt flow rate is more than 1, and
iii) maintaining the polypropylene obtained from step ii) at a temperature of at least 105° C. for a period of at least 48 hours.

2. The method of claim 1 wherein the FOG value as measured in accordance with VDA 278 of the polypropylene obtained after step iii) and having the target melt flow rate is at most 600 μg/g.

3. The method of claim 1 , wherein the target melt flow rate is from 20-70 g/10 min and/or wherein the initial melt flow rate is from 2-15 g/10 min.

4. The method of claim 1 , wherein the ratio of target to initial melt flow rate is at least 2.

5. The method of claim 1 , wherein the polypropylene is a heterophasic propylene copolymer.

6. The method of claim 1 , wherein the visbreaking is carried out using a peroxide.

7. A method for the manufacture of a reinforced polypropylene comprising the manufacture of polypropylene according to claim 1 , wherein a reinforcing filler is combined with the polypropylene obtained after step ii) and/or step iii).

8. The method of claim 7 wherein the polypropylene obtained after step ii) and/or step iii) and the reinforcing filler(s) are compounded in an extruder so as to form a polypropylene compound.

9. The method of claim 7 wherein the reinforced polypropylene is a fibre reinforced polypropylene and wherein the method further comprises applying a thermoplastic material comprising or consisting of the polypropylene obtained after step ii) or iii) as a sheath over said multifibre strand.

10. The method of claim 7 wherein the reinforced polypropylene is a fibre reinforced polypropylene and wherein the method further comprises pulling a continuous multifibre strand through a thermoplastic material comprising or consisting of the polypropylene obtained after step ii) or iii) in a molten state.

11. The method according to claim 9 , further comprising cutting the obtained pulltruded or sheathed continuous multifilament strand in pellets having a length of from 2-50 mm.

12. A thermoplastic composition obtainable by the method according to claim 7 .

13. Automotive interior article comprising the polypropylene obtainable by the method according to claim 1 .

14. The automotive interior article of claim 13 having an FOG value as measured in accordance with VDA 278 of at most at most 400 μg/g.

15. The automotive interior article of claim 13 having an FOG value as measured in accordance with VDA 278 of at most 250 μg/g.

16. The method of claim 2 , wherein FOG value is at most 400 μg/g.

17. The method of claim 16 , wherein the FOG value is at most 250 μg/g.

18. The method of claim 4 , wherein the ratio of target to initial melt flow rate is from 2 to 20.

19. The method of claim 18 , wherein the ratio of target to initial melt flow rate is from 4 to 10.

20. The method of claim 1 , wherein step ii) is carried out directly after step i).

Assignees

• Sabic Global Technologies Bv

Inventors

• Bercx Rick Robert Emilie
• Grein Christelle Marie Hélène

Classifications

• C08L2207/02

  Heterophasic composition · CPC title

• C08K7/14

  Glass · CPC title

• C08F8/50 Primary

  Partial depolymerisation · CPC title

• C08L23/14

  Copolymers of propene (C08L23/16 takes precedence) · CPC title

• C08L2023/42

  Depolymerisation, vis-breaking or degradation · CPC title